US4220511A - Treatment of sintered poly-tetrafluoroethylene with irradiation and heat to produce a grindable material - Google Patents
Treatment of sintered poly-tetrafluoroethylene with irradiation and heat to produce a grindable material Download PDFInfo
- Publication number
- US4220511A US4220511A US06/019,890 US1989079A US4220511A US 4220511 A US4220511 A US 4220511A US 1989079 A US1989079 A US 1989079A US 4220511 A US4220511 A US 4220511A
- Authority
- US
- United States
- Prior art keywords
- polytetrafluoroethylene
- irradiation
- sintered
- temperature
- mrads
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/28—Treatment by wave energy or particle radiation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/12—Powdering or granulating
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/3154—Of fluorinated addition polymer from unsaturated monomers
- Y10T428/31544—Addition polymer is perhalogenated
Definitions
- the present invention relates to processing of sintered polytetrafluoroethylene to render the material readily grindable to fine powders having low average particle size, 10 microns or less, and high melt flow characteristics.
- Polytetrafluoroethylene powders having particle sizes of 10 microns or less have been used for some time as lubricants in such materials as printing inks and in various fabrication processes.
- the sources of such powders are the various manufacturers of the material at current costs of $4.00 to $5.00 per pound unfabricated.
- the material may also be produced from scrap unsintered polytetrafluoroethylene currently purchasable at about $1.50 per pound. Unsintered scrap material however, is in short supply because only a small proportion of polytetrafluoroethylene is fabricated in the unsintered form.
- Sintered scrap polytetrafluoroethylene is in abundent supply at relatively low cost, currently about $0.40 per pound. However, the cost of converting sintered polytetrafluoroethylene into fine powder by prior art methods is prohibitive.
- Sintered polytetrafluoroethylene is known to degrade under ionizing irradiation and is grindable into fine powders of commercial interest, but only after exposure to irradiation levels in excess of 200 Mrads.
- Polytetrafluoroethylene is also known to be extremely stable under conditions of long term heat aging. For example, polytetrafluoroethylene is suitable as electrical insulation for continuous use up to 550° F. (288° C.). Discussions of the degradation of polytetrafluoroethylene under irradiation have been in the literature for many years. (See Charlesby--Chapter 20 and Chapiro pages 526 through 533). After exposure to very low doses ( ⁇ 5 Mrads), unsintered polytetrafluoroethylene can lose many of its desirable mechanical properties, even though it retains its chemical properties and remains inert for all practical purposes.
- the dose rates used in irradiating the polytetrafluoroethylene are those commonly experienced in using electron beam accelerators--e.g., ⁇ 1 Mrad/second.
- sintered polytetrafluoroethylene is nondestructively degraded to a degree necessary to render it grindable to fine powders, 10 microns or less, by irradiating the material in the presence of air or oxygen in a range of 45 Mrads to 200 Mrads, heating, either during or subsequent to irradiation, to temperatures in the range of 150° F. to 600° F. for a period of at least about one-half hour and grinding.
- the levels of irradiation required to lower the molecular weight of polytetrafluoroethylene can be materially reduced to a level rendering the process commercially viable.
- the upper temperature limit is the melting temperature of the material and may exceed 600° F. by a small percentage.
- the present invention is concerned with producing polytetrafluoroethylene powders capable of use as lubricants in inks and other commercial and industrial applications. Such powders must have a particle size of 10 microns or less and for purposes of this application such powders are referred to as "fine powders". Successful practice of the invention is achieved when fine powders are produced at costs that are economically competitive with other methods of producing such powders; a condition that could not be achieved prior to the present invention when using sintered polytetrafluoroethylene as the starting material.
- Materials produced may have an average particle size of less than 10 microns, a high melt flow or intermediate combinations depending on details of the treatment. The higher the temperature the more readily the material grinds to fine powder with less coarse particles. The longer the heat treatment at somewhat lesser temperatures the higher the melt flow and lower the molecular weight. Thus, a balance must be struck depending upon desired final characteristics. For instance an average particle size of 6.1 microns and melt flow at 330° C. of 1079 was obtained with a dose of 90 Mrads and a temperature of 500° F. held for 2 hours. An average particle size of 9.6 microns and a melt flow of 2136 at 330° C. was obtained with a dose of 90 Mrads, and a temperature of 500° F. held for 5 hours.
- irradiation heating and grinding may be conducted concurrently or successively. In the later case heating should occur before material loss of peroxidized or free radical species of polytetrafluoroethylene formed during irradiation, a matter of hours at least.
- FIG. 1 illustrates the statistical design of an experiment performed on two different lots of previously sintered polytetrafluoroethylene
- FIG. 2 is a plot of the effect of past irradiation heat treatment or melt flow of a first material
- FIG. 3 is a plot of the effect of post irradiation heat treatment or melt flow of a second material
- FIG. 4 is a plot of the effect of irradiation and heat treatment on average particle size of the first material
- FIG. 5 is a plot of the effect or irradiation and heat treatment on average particle size of the second material
- FIG. 6 is a plot of the effect of post irradiation heat treatment on large particles of the first material
- FIG. 7 is a plot of the effect of post irradiation heat treatment on large particles of the second material.
- solid sintered polytetrafluoroethylene scrap samples were exposed to electron beam radiation at beam acceleration voltage levels and dose rates as specified in each example.
- a sample of 100 grams of scrap flakes from previously sintered polytetrafluoroethylene was placed in a grinding device capable of simultaneously shredding the polymer and aerating it.
- This device consisted of a container with a high speed cutting blade at its base (a blender).
- the container with the scrap polytetrafluoroethylene in it was placed directly under an 800 KeV, 50 microamp electrom beam which produced an absorbed dose rate of 1.5 Mrad per minute.
- the material was exposed to a series of irradiation cycles which were followed by aeration cycles. During both cycles the grinding device was kept running. After a number of such cycles the polytetrafluoroethylene was found to grind to powder at surprisingly low doses.
- the polytetrafluoroethylene was contained within the grinding vessel. Although there were alternating cycles of aeration, heat was allowed to build up in the polymer. Although no direct temperature readings were made, 1 Mrad imparts ⁇ 10° C. (18° F.) to polytetrafluoroethylene (specific heat 0.25) and since the aeration and irradiation portions of a cycle were equal, the polytetrafluoroethylene being ground could not dissipate all of the heat generated from irradiation. Temperatures in the range of 300° F. to 500° F. are estimated.
- Example 2 Using the same irradiation conditions as in Example 1, that is with the grinder positioned directly under an 800 KeV, 50 microamp beam, fine powders were made from previously sintered polytetrafluoroethylene. In these runs samples were taken after different exposure levels. Distinct aeration steps were not included in the cycles; reliance being had on the effects of ambient air during irradiation. The scrap was simultaneously irradiated and ground with no cooling.
- melt rheological tests were run on the sintered polytetrafluoroethylene which had been simultaneously ground to fine powder while being irradiated. Using a capillary rheometer, melt viscosities were determined at 330° C. (626° F.). Under these conditions high molecular weight, non-irradiated polytetrafluoroethylene does not flow.
- the two samples were subject to different temperatures for different lengths of time.
- Example 1 Attempts were made to duplicate Example 1 using a 3.0 MeV electron beam accelerator. A larger blender was placed under the beam. A series of irradiation exposures were made concurrently grinding and irradiating previously sintered polytetrafluoroethylene. Each irradiation exposure was in 16 Mrad increments before polymer was inspected.
- the air mill relies on large particles impinging upon themselves in a high turbulence air stream in order for the particles to break themselves down. It is generally believed that an air mill can produce finer powders than a Hammermill. Both of these techniques are commercial methods for producing powders.
- the three axial coordinates of the design represent the three independent variables. Design points are chosen at the extremes for each independent variable, the ⁇ points, and at levels equal to the mid-point level plus or minuses the range divided by 3.364, the points designated ⁇ 1, ⁇ 1, ⁇ 1.
- the center point, 0, 0, 0, is chosen as the mid-point of these practical ranges which yield desirable results in earlier experiments. In order to estimate experimental error so that only significant interactions or relationships between properties and compositions are reported, six center point replicates are used.
- the data generated on each material was processed in a computer using step-wise multiple regression analysis.
- Such an analysis permits, on a statistical basis, a determination of the relative dependence of each of the dependent variables on the independent variables and on the interaction between two independent variables.
- the regression analysis also yields a correlation between each of the dependent variables thereby indicating whether one given test is closely related to another. For example:
- melt flow does not correlate well with the grindability of either material, especially in the ability to make fine powders.
- the regression analysis can be used to determine the relative dependence of each dependent variable or product property on the independent variables or process conditions.
- FIGS. 2-7 plot properties such as melt flow and average particle size against coordinates of dose and heat treating conditions.
- the non-linearity of these plots further exemplifies the dependence of the properties of powdered, low molecular weight polytetrafluoroethylene on heat treatment as well as irradiation.
- FIGS. 2 and 3 for Materials A and B, respectively, illustrate the time and temperature dependence of the heat treatment cycle on increasing the melt flow of the lower molecular weight polytetrafluoroethylene. Both figures illustrate that as dose increases, there is a corresponding increase in melt flow or molecular weight degradation.
- FIG. 2 shows that heat treating may be more effective at somewhat modest temperatures such as 150° C. or 302° C.; a temperature considerably below the upper temperature use limits for polytetrafluoroethylene. At such temperatures polytetrafluoroethylene is normally considered quite stable.
- FIGS. 4 and 5 for Materials A and B respectively show that the longer the post irradiation heat treatment cycle the more difficult it is to produce fine particles. Less time at temperature should lead to finer particle materials. The higher the temperature of the heat treatment the easier it appears to grind the material to fine powders. These inferences call for different heat treatment conditions, preferably a short duration exposure at high temperatures, say at 288° C. or 550° F., to produce finer particles. Longer heat treatment even at lower temperatures was indicated to lower molecular weight and increase melt flow. As noted above melt flow and the ability to grind degraded polytetrafluoroethylene to fine powders are not that closely correlated.
- FIGS. 6 and 7 for materials A and B respectively indicate that to avoid large particles or particle agglomerates it is desirable to use minimum duration heat treatment at maximum temperature; bearing in mind, for example, that Material B fused when conditioned at 600° F. (316° C.) and could not then be fed to a grinder.
- 600° F. 316° C.
- FIGS. 6 and 7 for materials A and B respectively indicate that to avoid large particles or particle agglomerates it is desirable to use minimum duration heat treatment at maximum temperature; bearing in mind, for example, that Material B fused when conditioned at 600° F. (316° C.) and could not then be fed to a grinder.
- 600° F. 316° C.
- FIGS. 6 and 7 for materials A and B respectively indicate that to avoid large particles or particle agglomerates it is desirable to use minimum duration heat treatment at maximum temperature; bearing in mind, for example, that Material B fused when conditioned at 600° F. (316° C.) and could not then be fed to a grinder.
- polytetrafluoroethylene is well known for its thermal stability at the temperatures to which it was exposed during concurrent irradiation and grinding and during post-irradiation heat treatment. Since air and/or oxygen are needed for degradation of polytetrafluoroethylene, it would appear that while irradiation directly account for substantial degradation of polytetrafluoroethylene, it also produces oxidized or peroxidized polytetrafluorethylene.
- Such polytetrafluoroethylene and polytetrafluoroethylene with free radicals still present must exist for at least several hours after irradiation.
- Post irradiation heat treatment consumes these peroxidized or free radical species of polytetrafluoroethylene and leads to further molecular weight reduction.
- free radical and peroxidation reactions are time/temperature dependent and are accelerated by exposure to elevated temperatures.
- the morphology of crystalline polymers as polytetrafluoroethylene can also be affected by exposure to elevated temperatures below their melt transition.
- Time of heating is a factor which is determined not only by effects on particle size but also the time required to remove from the plastic by diffusion through the plastic, of free fluorene liberated during the irradiation cycle. At present this latter factor has somewhat restricted the lower limit of processing times although processing times of one-half hour are believed to be valid to accomplish sufficient treatment of sintered polytetrafluoroethylene to permit grinding to fine powders.
Abstract
Sintered polytetrafluoroethylene is nondestructively degraded so as to be grindable to a powder of an average size of less than 10 microns by a combination of irradiation by electrons or other subatomic particles in the presence of oxygen or air and concurrent or subsequent heating at temperatures below the melting point of the material. The preferred effective and economic range of irradiation, heat and time at temperature is approximately 50-150 Mrads, 150° F. to 600° F. for at least about one-half hour depending upon desired average particle size and melt flow characteristics and acceptable yields of fine powders.
Description
The present invention relates to processing of sintered polytetrafluoroethylene to render the material readily grindable to fine powders having low average particle size, 10 microns or less, and high melt flow characteristics.
Polytetrafluoroethylene powders having particle sizes of 10 microns or less have been used for some time as lubricants in such materials as printing inks and in various fabrication processes. The sources of such powders are the various manufacturers of the material at current costs of $4.00 to $5.00 per pound unfabricated. The material may also be produced from scrap unsintered polytetrafluoroethylene currently purchasable at about $1.50 per pound. Unsintered scrap material however, is in short supply because only a small proportion of polytetrafluoroethylene is fabricated in the unsintered form.
Sintered scrap polytetrafluoroethylene is in abundent supply at relatively low cost, currently about $0.40 per pound. However, the cost of converting sintered polytetrafluoroethylene into fine powder by prior art methods is prohibitive.
Sintered polytetrafluoroethylene is known to degrade under ionizing irradiation and is grindable into fine powders of commercial interest, but only after exposure to irradiation levels in excess of 200 Mrads. Polytetrafluoroethylene is also known to be extremely stable under conditions of long term heat aging. For example, polytetrafluoroethylene is suitable as electrical insulation for continuous use up to 550° F. (288° C.). Discussions of the degradation of polytetrafluoroethylene under irradiation have been in the literature for many years. (See Charlesby--Chapter 20 and Chapiro pages 526 through 533). After exposure to very low doses (˜5 Mrads), unsintered polytetrafluoroethylene can lose many of its desirable mechanical properties, even though it retains its chemical properties and remains inert for all practical purposes.
Surprisingly it has been found that a combination of irradiation and heat significantly affects the degradation of sintered polytetrafluoroethylene. Under normal circumstances polytetrafluoroethylene which has been sintered (exposed for ˜5 minutes at 800° F. or 427° C.) does not readily degrade under irradiation. However, either by concurrently irradiating and heating or by irradiating and then heating, it has been found that the levels of irradiation required to lower the molecular weight of polytetrafluoroethylene can be substantially reduced. This can be accomplished at temperatures significantly below the melt transition of polytetrafluoroethylene (342° C. or 648° F.) and at temperatures (i.e. <550° F. or 288° C.) where polytetrafluoroethylene is normally considered quite stable. Furthermore, the dose rates used in irradiating the polytetrafluoroethylene are those commonly experienced in using electron beam accelerators--e.g., ˜1 Mrad/second.
Dillin, U.S. Pat. No. 3,766,031, has suggested that sintered polytetrafluoroethylene can be degraded by irradiation at dose levels in the ranges of from about 5 Mrads to 25 mrads with heating not to exceed 250° F. Experiments performed using such techniques failed to permit sintered polytetrafluoroethylene to be ground to particle sizes noted in the patent. In fact with doses of from 10-25 Mrads and temperatures from 213° F.-248° F. no powders were produced. Some coarse powder was produced when the upper irradiation level of the patent were exceeded by about 60%, but no powders were produced when the temperature range was exceeded but the irradiation was held within range.
According to the present invention sintered polytetrafluoroethylene is nondestructively degraded to a degree necessary to render it grindable to fine powders, 10 microns or less, by irradiating the material in the presence of air or oxygen in a range of 45 Mrads to 200 Mrads, heating, either during or subsequent to irradiation, to temperatures in the range of 150° F. to 600° F. for a period of at least about one-half hour and grinding. Surprisingly, it has been found that by utilizing a combination of irradiation, at doses normally considered low and heating in ranges at which polytetrafluoroethylene is normally stable, the levels of irradiation required to lower the molecular weight of polytetrafluoroethylene can be materially reduced to a level rendering the process commercially viable. It should be noted that the upper temperature limit is the melting temperature of the material and may exceed 600° F. by a small percentage.
The present invention is concerned with producing polytetrafluoroethylene powders capable of use as lubricants in inks and other commercial and industrial applications. Such powders must have a particle size of 10 microns or less and for purposes of this application such powders are referred to as "fine powders". Successful practice of the invention is achieved when fine powders are produced at costs that are economically competitive with other methods of producing such powders; a condition that could not be achieved prior to the present invention when using sintered polytetrafluoroethylene as the starting material.
It has been found that production of powders on a batch basis in accordance with the teachings of the present invention generally results in a material having a large proportion of fine powder, some coarse powder (above 10 microns) and some coarse material above, for instance, 60 microns.
In determining whether a particular process is successful when practiced on a batch basis, the economics of the situation must be considered as determined by the following factors; the cost of the new material, the cost of processing (irradiation, heating and grinding), and the yield which determines the total cost per pound of fine powder. As the economics of the industry changes the yields related to a "successful" process must as a practical matter, vary. At the present time a process of the present invention that yields a material with a mear particle size of 10 microns or less is considered eminently economically successful.
In commercial practice a continuous process will normally be employed. In such a process, it is envisioned that material will be spread on a conveyor, passed under an electron beam, concurrently and/or subsequently passed through an air circulating oven at a speed such that the material is subjected to the desired heat for the desired time period. The material thereafter will pass into a grinder, probably an air mill, and dispensed therefrom through an air stream that belows off the particles of 10 microns or less (for collection) while the remaining materials are collected and dispersed again or the conveyor with new scrap for additional irradiation, heating and grinding.
In the continuous processing case yields approaching 100% should be attained and an economic process is then determined by the yield per hour relative to total cost per hour.
Materials produced may have an average particle size of less than 10 microns, a high melt flow or intermediate combinations depending on details of the treatment. The higher the temperature the more readily the material grinds to fine powder with less coarse particles. The longer the heat treatment at somewhat lesser temperatures the higher the melt flow and lower the molecular weight. Thus, a balance must be struck depending upon desired final characteristics. For instance an average particle size of 6.1 microns and melt flow at 330° C. of 1079 was obtained with a dose of 90 Mrads and a temperature of 500° F. held for 2 hours. An average particle size of 9.6 microns and a melt flow of 2136 at 330° C. was obtained with a dose of 90 Mrads, and a temperature of 500° F. held for 5 hours.
As indicated, irradiation heating and grinding may be conducted concurrently or successively. In the later case heating should occur before material loss of peroxidized or free radical species of polytetrafluoroethylene formed during irradiation, a matter of hours at least.
FIG. 1 illustrates the statistical design of an experiment performed on two different lots of previously sintered polytetrafluoroethylene;
FIG. 2 is a plot of the effect of past irradiation heat treatment or melt flow of a first material;
FIG. 3 is a plot of the effect of post irradiation heat treatment or melt flow of a second material;
FIG. 4 is a plot of the effect of irradiation and heat treatment on average particle size of the first material;
FIG. 5 is a plot of the effect or irradiation and heat treatment on average particle size of the second material;
FIG. 6 is a plot of the effect of post irradiation heat treatment on large particles of the first material;
FIG. 7 is a plot of the effect of post irradiation heat treatment on large particles of the second material.
In the following examples, solid sintered polytetrafluoroethylene scrap samples were exposed to electron beam radiation at beam acceleration voltage levels and dose rates as specified in each example.
A sample of 100 grams of scrap flakes from previously sintered polytetrafluoroethylene was placed in a grinding device capable of simultaneously shredding the polymer and aerating it. This device consisted of a container with a high speed cutting blade at its base (a blender). The container with the scrap polytetrafluoroethylene in it was placed directly under an 800 KeV, 50 microamp electrom beam which produced an absorbed dose rate of 1.5 Mrad per minute. The material was exposed to a series of irradiation cycles which were followed by aeration cycles. During both cycles the grinding device was kept running. After a number of such cycles the polytetrafluoroethylene was found to grind to powder at surprisingly low doses.
______________________________________
Cumul-
Cy- ative
cle Condition of Ground Material
Dose
______________________________________
1 White flakes 3 Mrads
2 White flakes 6 Mrads
3 Flakes with some fines 12 Mrads
4 Flakes with some fines and some visible powder
24 Mrads
5 More loosely packed fines 24 Mrads
6 Mixture of coarse fines and some powder
30 Mrads
7 Powdered 42 Mrads
8 Fine powder 54 Mrads
______________________________________
During the entire run, the polytetrafluoroethylene was contained within the grinding vessel. Although there were alternating cycles of aeration, heat was allowed to build up in the polymer. Although no direct temperature readings were made, 1 Mrad imparts ˜10° C. (18° F.) to polytetrafluoroethylene (specific heat 0.25) and since the aeration and irradiation portions of a cycle were equal, the polytetrafluoroethylene being ground could not dissipate all of the heat generated from irradiation. Temperatures in the range of 300° F. to 500° F. are estimated.
Using the same irradiation conditions as in Example 1, that is with the grinder positioned directly under an 800 KeV, 50 microamp beam, fine powders were made from previously sintered polytetrafluoroethylene. In these runs samples were taken after different exposure levels. Distinct aeration steps were not included in the cycles; reliance being had on the effects of ambient air during irradiation. The scrap was simultaneously irradiated and ground with no cooling.
______________________________________
Sintered PTFE
Dose Condition of Material
______________________________________
24 Mrads Mixture of fine and coarse particles
30 Mrads Fine powder collecting on walls of vessel
36 Mrads Fewer coarse particles
48 Mrads Mostly powder; some coarse particles
54 Mrads Very fine powder
66 Mrads Very fine powder, less coarse particles
78 Mrads Very fine powder (about the same as 66 Mrads)
______________________________________
Melt rheological tests were run on the sintered polytetrafluoroethylene which had been simultaneously ground to fine powder while being irradiated. Using a capillary rheometer, melt viscosities were determined at 330° C. (626° F.). Under these conditions high molecular weight, non-irradiated polytetrafluoroethylene does not flow.
______________________________________
Cumulative
Apparent Shear
Material Dose Melt Viscosity
Rate
______________________________________
Sintered PTFE
78 Mrads 591 poises 417 sec.sup.-1
powder
(2 different samples) 401 poises 1389 sec.sup.-1
______________________________________
The two samples were subject to different temperatures for different lengths of time.
In an attempt to isolate the effects of irradiation from those of heat and grinding, previously sintered polytetrafluoroethylene chips were irradiated in air using a 3 MeV, 33 milliamp accelerator; a Dynamitron® manufactured by Radiation Dynamics, Inc. Samples were taken at different intervals and then ground 30 seconds after each irradiation cycle. Dose was accumulated in 1.5 Mrad increments. After a 10 Mrad accumulation, material was ground and then allowed to cool for at least 10 minutes before receiving any additional exposure to irradiation. This experiment showed that exceedingly high doses were required to render sintered polytetrafluoroethylene grindable to fine powder when the polymer did not develop or retain any heat history; i.e. effectively was not heat treated.
______________________________________
Sintered PTFE
Dose Condition of Ground Material
______________________________________
Series A 30 Mrads Chips - no effect
40 Mrads Chips - no effect
50 Mrads Chips - no effect
60 Mrads Chips - no effect
70 Mrads Chips - no effect
Series B
100 Mrads Chips - slight powder
110 Mrads Chips and some powder
120 Mrads Chips and some powder
130 Mrads Chips and some powder
140 Mrads Chips and some powder
Series C
200 Mrads Coarse powder, some fines
210 Mrads Powder, some coarse particles
220 Mrads Powder, fewer coarse particles
230 Mrads Powder, fewer coarse particles
240 Mrads Powder, fewer coarse particles
______________________________________
Without concurrent heating, as in Examples 1 and 2, it took over 200 Mrads to mechanically reduce previously sintered polytetrafluoroethylene to a fine powder when the polymer was allowed to cool after irradiation steps. In no instance was fine powder produced in quantities that are considered economic yields. Not only weren't the yields in the above process not economic but the times involved were prohibitive. For instance if 240 Mrads were applied without interruption temperatures of 2400° F. would be generated in the material. At all times of course, the temperature must be held below the melting point of the polytetrafluoroethylene and thus cooling times between irradiation cycles are great, at least 10 minutes as stated above. Thus irradiation periods in excess of 7 hours were encountered.
Attempts were made to duplicate Example 1 using a 3.0 MeV electron beam accelerator. A larger blender was placed under the beam. A series of irradiation exposures were made concurrently grinding and irradiating previously sintered polytetrafluoroethylene. Each irradiation exposure was in 16 Mrad increments before polymer was inspected.
______________________________________ Dose Condition of Ground Material ______________________________________ 16 Mrads No powder 32 Mrads Coarse pieces, no powder 48 Mrads Some fine powder ______________________________________
This run was terminated because the heat build up in the polytetrafluoroethylene was sufficient to melt the plastic walls of the blender used in grinding.
To understand the influence of grinding while irradiating, two identical grinders or blenders were placed under the 3.0 MeV beam. One was set up with a commercial grinding blade capable of running at ˜20,000 rpm. The second had paddle stirring blades and operated at only 68 rpm. Both blenders were filled with the same amount of previously sintered polytetrafluoroethylene. Irradiation was carried out in 4 Mrad increments. High speed grinding and simple stirring were both able to produce fine powdered polytetrafluoroethylene. As would be expected the higher speed grinding yielded a slightly finer powder.
______________________________________
Condition of Ground Material
Dose High Speed Low Speed
______________________________________
20 Mrad Slight powder Slight powder
52 Mrad Significant powder
Significant powder
80 Mrad Less coarse powder
Slightly more coarse
______________________________________
During both grinding operations the powder was very hot, probably between 200° C. and 250° C. (392° F. and 482° F.).
In order to better understand the factors influencing the irradiation degradation of previously sintered polytetrafluoroethylene, the experimental chamber used in Examples 1 and 2 was modified so that a controlled environment could be introduced into the grinder or blender. All trial runs were carried out using the 800 KeV 50 microamp electron beam accelerator with material being simultaneously irradiated and ground.
______________________________________
Environment Dose Condition of Ground Material
______________________________________
Ambient air
45% RH 80 Mrads Fine powder
Moist oxygen
80% RH 48 Mrads Greasy powder (not as fine)
80 Mrads Fine powder
Moist nitrogen
76% RH 80 Mrads Could not be ground
______________________________________
Thus air or oxygen must be present during the irradiation degradation of polytetrafluoroethylene.
Since the presence of heat and oxygen contributed to the irradiation degradation of polytetrafluoroethylene a series of experiments was run to determine if heating the polytetrafluoroethylene after irradiation could produce some of the beneficial effects observed from concurrently irradiating, heating and grinding polytetrafluoroethylene.
______________________________________
Heat
Treat- Sintered PTFE
Dose ment Condition of Ground Material
______________________________________
200 Mrads
None Mixture of fine and coarse particles
200 Mrads
5 hours Mixture of fine and some coarse particles.
at 550° F.
Notably less coarse particles than either
(288° C.)
of others in this example.
50 Mrads
1 hour at
Fine powder, some coarse particles.
550° F.
(288° C.)
______________________________________
The fine and coarse particles from the 50 Mrad sintered polytetrafluoroethylene exposed for 1 hour at 550° F. (288° C.) were separated. Melt viscosity showed the fines were somewhat lower in molecular weight. Using a capillary rheometer at 330° C. (626° F.), these data were obtained:
______________________________________
Sample Shear Rate Apparent Melt Viscosity
______________________________________
Coarse particles
139 sec.sup.-1
1940 poises
417 sec.sup.-1
1225 poises
1389 sec.sup.-1
735 poises
Fine particles
139 sec.sup.-1
491 poises
417 see.sup.-1
320 poises
1389 sec.sup.-1
200 poises
______________________________________
This data may reflect that grinding in a blender in itself separates the materials by molecular weight with the lower molecular weight (lower melt viscosity) polytetrafluoroethylene being easier to grind. It is apparent from this Example that irradiation and heating are not required to occur simultaneously, an important point since in commercial practice separation of the irradiation, heating and grinding operation may be desirable.
In all of the previous examples grinding of polytetrafluoroethylene was carried out in a blender-type grinder. Irradiation exposure in most cases was concurrent with grinding. Since it was shown in Example 7 that post heating of irradiated sintered polytetrafluoroethylene scrap could also produce low molecular weight polytetrafluoroethylene capable of being ground to fine powder, it was then possible to irradiate, then heat treat sintered polytetrafluoroethylene scrap and then subsequently grind it to powder using commercial, continuous grinding equipment. Using sintered polytetrafluoroethylene scrap, a series of runs was made using a Hammermill with a 0.027 inch round screen.
______________________________________
Condition of
Dose Heat Treatment Ground Material
______________________________________
80 Mrads
6 hours at 550° F. (288° C.)
Fine powder
100 Mrads
6 hours at 550° F. (288° C.)
Fine powder
200 Mrads
6 hours at 550° F. (288° C.)
Fine powder
200 Mrads
None Hard granular
material, little powder
______________________________________
Heretofore, all of the comparisons made on the grindability of irradiation degraded polytetrafluoroethylene have been based on visual observation and visual comparisons. To quantify the particle size of the various ground powders, these materials were subjected to analysis in a Coulter Counter manufactured by Coulter Electronics, Inc., Model No. TA-II, which is an electronic device capable of measuring particle size and plotting particle size distributions. Previously sintered polytetrafluoroethylene was irradiated to several doses, then heat treated and then ground in an air mill, Jet Pulverizer's Micro Master®. The Hammermill relies on breaking down materials to fine powders by mechanically pounding large particles between metal plates and then allowing fine particles to pass through a screen. The air mill relies on large particles impinging upon themselves in a high turbulence air stream in order for the particles to break themselves down. It is generally believed that an air mill can produce finer powders than a Hammermill. Both of these techniques are commercial methods for producing powders.
______________________________________
Coulter Counter Particles Size
Percent
<2 >30 >60
Dose Heat Treatment
Average micron
micron
micron
______________________________________
80 6 hours at 550° F.
6.4 3.0% 2.5% 0%
Mrad (288° C.)
microns
100 6 hours at 550° F.
6.6 4.0% 7.5% 5.0%
Mrad (288° C.)
microns
200 6 hours at 550° F.
4.7 8.0% 4.0% 2.0%
Mrad (288° C.)
microns
250 None 5.1 7.0% 5.0% 1.5%
Mrad microns
______________________________________
All of these materials were processed at 3 pounds per hour using a 4 inch diameter air mill. From this data it can be clearly seen that a combination of moderate irradiation degradation (80 Mrads) when coupled with a heat treatment can produce grindable polytetrafluoroethylene from previously sintered scrap. Particle sizes comparable to ones obtained after very high exposures (250 Mrads) can be had. However, all samples had some large chunks (>64 microns) which were ignored by the Coulter counter.
To further characterize the influence of irradiation and heat treatment on the degradation of previously sintered polytetrafluoroethylene scrap, a series of materials were prepared at different doses and heat treatments. These were then ground in a 12 inch diameter air mill at a rate of 10 pounds per hour.
______________________________________
Coulter Counter Particle
Size Percent
Dose Heat Treatment Average <2.0 μ
>60.0 μ
______________________________________
60 6 hours at 550° F.(288° C.)
4.7 10.0% 4.0%
Mrads microns
80 6 hours at 550° F.(288° C.)
4.4 10.0% 4.0%
Mrads microns
100 6 hours at 550° F.(288° C.)
4.8 8.0% 1.0%
Mrads microns
60 1 hour at 550° F.(288° C.)
6.7 6.0% 5.0%
Mrads microns
100 1 hour at 550° F.(288° C.)
6.3 8.0% 2.0%
Mrads microns
______________________________________
It is apparent that over a moderate dose range, 60 through 100 Mrads, previously sintered polytetrafluoroethylene can be degraded and made grindable into fine powders when post heated for anywhere between 1 and 6 hours at an elevated temperature.
In order to more thoroughly understand the influence of irradiation dose and heat treatment on the degradation and grindability of previously sintered polytetrafluoroethylene scrap, a statistically designed experiment was run on two different lots of previously sintered polytetrafluoroethylene. This type of designed experiment is known as a central composite design for three independent variables. (See "Applications of Statistics to Experimentation" by J. S. Hunter, presented to the AICHE meeting Apr. 20-23, 1958.)
In this experiment, three parameters affecting the degradation of sintered polytetrafluoroethylene were allowed to vary:
______________________________________ Independent Variables Range ______________________________________ 1.Radiation dose 0 to 115Mrads 2. Temperature of heat treatment 100° F. to 600° F. (38° C. to 316° C.) 3. Time attemperature 1 hour to 6 hours ______________________________________
This covers a broad, but practical range of irradiation dose, temperature of heat treatment and time for post-irradiation heat treatment.
The design for this type of experiment is illustrated in FIG. 1 of the accompanying drawings.
The three axial coordinates of the design represent the three independent variables. Design points are chosen at the extremes for each independent variable, the α points, and at levels equal to the mid-point level plus or minuses the range divided by 3.364, the points designated ±1, ±1, ±1. The center point, 0, 0, 0, is chosen as the mid-point of these practical ranges which yield desirable results in earlier experiments. In order to estimate experimental error so that only significant interactions or relationships between properties and compositions are reported, six center point replicates are used.
The dependent variables or tests performed on each material produced at the various combinations of dose, temperature and time at temperature were:
1. Melt flow rate--determined using a melt index tester at 330° C. (626° F.) with 2160 gram load. This temperature and load combination was found to give good results with polytetrafluoroethylene.
2. Average particle size--determined from Coulter Counter readings of particle size distribution.
3. Percent of particles less than 20 microns--determined from Coulter counter readings.
4. Percent of particles less than 75 microns--determined by weight percent which would pass through a 100 mesh screen. Since the Coulter counter can sometimes ignore or fail to take into its count very large particles, this alternate method of particle size determination was made.
All materials were irradiated to the prescribed dose using a 3 MeV electron beam accelerator. Materials were irradiated in air on open trays. After irradiation, test samples were placed in an air circulating laboratory oven capable of maintaning the desired temperature to ±1° C. Grinding to fine powders was accomplished using a 4 inch diameter air mill with a feed rate of 5 pounds per hour. In the following samples, Material A is pure sintered polytetrafluoroethylene scrap and Material B is sintered scrap polytetrafluoroethylene which had process oil incorporated therein to enhance its extrusion properties.
The tables below summarize the test conditions and data obtained.
TABLE I
__________________________________________________________________________
SINTERED PTFE - MATERIAL A
Design Matrix Position:
111
11-1
1-11
1-1-1
111
11-1
1-11
1-1-1
__________________________________________________________________________
Independent Variables
Dose, in Mrads:
90 90 90 90 25 25 25 25
Temperature, °F.:
500
500
200
200
500
500
200
200
Time at temperature, hours:
5 2 5 2 5 2 5 2
Dependent Variables
Melt flow at 330° C.:
154
1079
598
1162
17 0.02
0.7
3.0
Average particle size, μ:
15 6.1
8.6
16 21 19 14 17
Percent <20 microns:
67 87 86 62 47 55 70 61
Percent <75 microns:
39 76 47 27 24 8 6 2
(by screening)
__________________________________________________________________________
TABLE II
__________________________________________________________________________
SINTERED PTFE - MATERIAL A (Continued)
Extreme Points
Design Matrix Position:
+α,0,0
-α, 0,0
0,+<,0
0,- α0
0,0,+ α
0,0,-α
__________________________________________________________________________
Independent Variables
Dose, in Mrads:
115 0 60 60 60 60
Temperature, °F.:
350 350 600 100 350 350
Time at temperature, hours:
3.5 3.5 3.5 3.5 6 1
Dependent Variables
Melt flow at 330° C.:
1783
0 176 239 215 61
Average particle size, μ:
14 -- 11 13 21 20
Percent <20 microns:
64 -- 74 71 48 50
Percent <75 microns:
50 -- 35 23 16 8
(by screening)
__________________________________________________________________________
Point -α,0,0 with no irradiation did not flow in the melt flow test
and could not be ground.
TABLE III
__________________________________________________________________________
SINTERED PTFE - MATERIAL A (Continued)
Center Point Replicates
Design Matrix Position:
0,0,0
0,0,0
0,0,0
0,0,0
0,0,0
0,0,0
__________________________________________________________________________
Independent Variables:
Dose, in Mrads:
60 60 60 60 60 60
Temperature, °F.:
350 350 350 350 350 350
Time at temperature, hours:
3.5 3.5 3.5 3.5 3.5 3.5
Dependent Variables
Melt flow at 330° C.:
193 80 215 159 188 268
Average particle size, μ:
16 15 13 21 12 17
Percent <20 microns:
61 67 73 49 81 62
Percent <75 microns:
16 14 19 14 23 26
(By screening)
__________________________________________________________________________
TABLE IV
__________________________________________________________________________
SINTERED PTFE - MATERIAL B
Third Order Factorial Points
Design Matrix Position:
111
11-1
1-11
1-1-1
111
11-1
1-11
1-1-1
__________________________________________________________________________
Independent Variables
Dose, in Mrads:
90 90 90 90 25 25 25 25
Temperature, °F.:
500
200
500
200
500
200
500
200
Time at temperature, hours:
5 2 5 2 5 2 5 2
Dependent Variables
Melt flow at 330° C.:
2136
141
978
993
51 2.2
0.5
3.3
Average particle size, μ:
9.6
7.6
9.0
9.8
18 19 17 24
Percent <20 microns:
82 78 83 87 59 56 62 42
Percent <75 microns
95 77 61 82 56 27 33 23
(By screening)
__________________________________________________________________________
TABLE V
__________________________________________________________________________
SINTERED PTFE - MATERIAL B (Continued)
Extreme Points
Design Matrix Position:
+α ,0,0
-α,0,0
0,+α,0
0,-α,0
0,0,+ α
0,0,-α
__________________________________________________________________________
Independent Variables
Dose, in Mrads:
115 0 60 60 60 60
Temperature, °F.:
350 350 600 100 350 350
Time at temperature, hours:
3.5 3.5 3.5 3.5 6 1
Dependent Variables
Melt flow at 330° C.:
2130
0 5.4 91 51 158
Average particle size, μ:
11 -- -- 14 19 26
Percent <20 microns:
72 -- -- 76 52 38
Percent <75 microns:
69 -- -- 43 37 39
(By screening)
__________________________________________________________________________
Point -α,0,0 with no irradiation did not flow in the melt flow test
and could not be ground.
Point 0,+α ,0 with high temperature exposure agglomerated in the
oven and could not be fed to the grinder.
TABLE VI
______________________________________
SINTERED PTFE - MATERIAL B (Continued)
Center Point Replicates
Design Matrix Position:
0,0,0 0,0,0 0,0,0
0,0,0
0,0,0
0,0,0
______________________________________
Independent Variables
Dose, in Mrads:
60 60 60 60 60 60
Temperature, °F.:
350 350 350 350 350 350
Time at temperature,
3.5 3.5 3.5 3.5 3.5 3.5
hours:
Dependent Variables
Melt flow at 330° C.:
72 230 179 152 157 145
Average particle size, μ:
21 20 19 12 13 18
Percent <20 microns:
48 50 54 71 78 59
Percent <75 microns:
37 46 50 39 58 49
(By screening)
______________________________________
The data generated on each material was processed in a computer using step-wise multiple regression analysis. Such an analysis permits, on a statistical basis, a determination of the relative dependence of each of the dependent variables on the independent variables and on the interaction between two independent variables. The regression analysis also yields a correlation between each of the dependent variables thereby indicating whether one given test is closely related to another. For example:
TABLE VII
______________________________________
Material A - Inter-Relationship
of Test Methods
Correlation Matrix Giving Correlation Coefficients
Average
Part-
Melt icle Percent
Percent
Flow size <20μ
<75μ
______________________________________
Melt Flow 1.00
Average Particle Size
.41 1.00
Percent <20μ
.33 .96 1.00
Percent <75μ
.71 .69 .64 1.00
______________________________________
Material B - Inter-Relationship
of Test Methods
Correlation of Matrix Giving Correlation Coefficients
Average
Part-
Melt icle Percent
Percent
Flow size <20μ
<75μ
______________________________________
Melt Flow 1.00
Average Particle Size
.55 1.00
Percent <20μ
.56 .95 1.00
Percent <75μ
______________________________________
From both sets of correlation coefficients, it can be seen that melt flow does not correlate well with the grindability of either material, especially in the ability to make fine powders. There is a stronger correlation (0.71 and 0.73) between melt flow and the ability to grind materials without producing large agglomerates or particle chunks which could not pass through a screen. There is a very high correlation between the two pieces of information gathered from Coulter counter curves on particle size distribution. This probably reflects the normalacy of the Coulter curves. There is only a fair correlation between particle data generated from the Coulter counter and that obtained by screening. This probably reflects the Coulter counter's neglect of very large agglomerates or particles, which screening does not.
More important, however, the regression analysis can be used to determine the relative dependence of each dependent variable or product property on the independent variables or process conditions. The greater the correlation between a statistical variation in a given property and a variation in a process condition, the more it can be said that said process condition controls or can be used to control a given property. Since the design of the process conditions (independent variables) used to produce low molecular weight, powdered polytetrafluoroethylene from previously sintered polytetrafluoroethylene was statistically based, the results and inferences from them cannot be ascribed to randon experimental behavior.
For each material, the step-wise regression analysis of the data from the central composite designed experiment, indicates the dependence of properties on process conditions. The information presented below demonstrates that irradiation alone cannot account for the degradation and grindability of previously sintered polytetrafluoroethylene. Exposure to temperatures at which polytetrafluoroethylene is normally considered stable accounts for some of the degradation and grindability of the previously sintered polytetrafluoroethylene.
TABLE VIII
__________________________________________________________________________
SINTERED PTFE - MATERIAL A
Designed Experiment Step-Wise Regression Analysis
Independent Variables - Process Conditions
Dependent Variables
(Total Variance Explained)
Product Properties
Dominant Factor
Secondary Factor
Tertiary Factor
__________________________________________________________________________
Melt Flow Dose (77%) Interaction of dose and
Time at tempera-
time at temperature (87%)
ture (91%)
Average Particle Size
Dose (45%) Time at temperature (66%)
Temperature (72%)
Percent <20 microns
Dose (31%) Temperature (55%)
Time at tempera-
ture (63%)
Percent <75 microns
Interaction of dose
Dose (69%) Temperature (76%)
(By screening)
and temperature (60%)
__________________________________________________________________________
TABLE IX
__________________________________________________________________________
SINTERED PTFE - MATERIAL B
Designed Experiment Step-Wise Regression Analysis
Independent Variables - Process Conditions
Dependent Variables
(Total Variance Explained)
Product Properties
Dominant Factor
Secondary Factor
Tertiary Factor
__________________________________________________________________________
Melt Flow Dose (75%)
Interaction of dose and
Temperature (86%)
time at temperature (81%)
Average Particle Size
Dose (55%)
Temperature (61%)
Time at tempera-
ture (65%)
Percent <20 microns
Dose (42%)
Interaction of dose and
Time at tempera-
temperature (47%)
ture (52%)
Percent <75 microns
Dose (63%)
Temperature (68%)
Interaction of
(By screening) temperature and
time at tempera-
ture (71%)
__________________________________________________________________________
For both previously sintered polytetrafluoroethylene materials, the extent of irradiation dominates the degradation as indicated by increased melt flow and the ability to grind the degraded polytetrafluoroethylene into powders. However, in both cases heat treating plays a significant role. Heat treating irradiated polytetrafluoroethylene has considerable impact, especially with Material A, on the ability to grind these materials to fine powders. For Material A, irradiation only accounts for 45% of the variance in average particle size; whereas heat treating accounts for at least another 27% of the variance. This data clearly demonstrates a significant dependence of grindability on heat treating irradiated polytetrafluoroethylene which had been previously sintered.
Another way to indicate the relative dependence of the properties of irradiation degraded previously sintered polytetrafluoroethylene is to use the regression equations developed in the regression analysis in a contour plotting program. The accompanying FIGS. 2-7 plot properties such as melt flow and average particle size against coordinates of dose and heat treating conditions. The non-linearity of these plots further exemplifies the dependence of the properties of powdered, low molecular weight polytetrafluoroethylene on heat treatment as well as irradiation.
FIGS. 2 and 3 for Materials A and B, respectively, illustrate the time and temperature dependence of the heat treatment cycle on increasing the melt flow of the lower molecular weight polytetrafluoroethylene. Both figures illustrate that as dose increases, there is a corresponding increase in melt flow or molecular weight degradation. FIG. 2 shows that heat treating may be more effective at somewhat modest temperatures such as 150° C. or 302° C.; a temperature considerably below the upper temperature use limits for polytetrafluoroethylene. At such temperatures polytetrafluoroethylene is normally considered quite stable.
On the other hand, FIGS. 4 and 5 for Materials A and B respectively, show that the longer the post irradiation heat treatment cycle the more difficult it is to produce fine particles. Less time at temperature should lead to finer particle materials. The higher the temperature of the heat treatment the easier it appears to grind the material to fine powders. These inferences call for different heat treatment conditions, preferably a short duration exposure at high temperatures, say at 288° C. or 550° F., to produce finer particles. Longer heat treatment even at lower temperatures was indicated to lower molecular weight and increase melt flow. As noted above melt flow and the ability to grind degraded polytetrafluoroethylene to fine powders are not that closely correlated.
FIGS. 6 and 7 for materials A and B respectively indicate that to avoid large particles or particle agglomerates it is desirable to use minimum duration heat treatment at maximum temperature; bearing in mind, for example, that Material B fused when conditioned at 600° F. (316° C.) and could not then be fed to a grinder. For Material A (FIG. 6) higher temperatures yielded material free from large particles at lower doses. For Material B (FIG. 7) higher irradiation doses are indicated when using high temperatures to avoid large particles. These two figures are based on the extrapolation of data generated from screening the ground polytetrafluoroethylene for large particles, not on Coulter counter data.
Interpolating the information provided by these figures an optimum set of process conditions can be derived for the irradiation degradation and heat treatment of previously sintered polytetrafluoroethylene which is to be ground into fine powders. The duration and temperature of the heat treating cycle depends on the balance of particle size and molecular weight (melt flow) desired in a final product. It is apparent that post irradiation heat treatment is useful both in degrading previously sintered polytetrafluoroethylene and in rendering such material grindable into fine powders.
The mechanisms involved in rendered sintered polytetrafluoroethylene grindable into fine powders are not fully understood and the following attempt at explanation is not necessarily correct, but does appear to explain the observed facts.
The fact that a concurrent or post irradiation heat treatment of irradiated polytetrafluoroethylene is efficacious in reducing the molecular weight of polytetrafluoroethylene and in rendering it grindable is quite surprising. As noted hereinabove, polytetrafluoroethylene is well known for its thermal stability at the temperatures to which it was exposed during concurrent irradiation and grinding and during post-irradiation heat treatment. Since air and/or oxygen are needed for degradation of polytetrafluoroethylene, it would appear that while irradiation directly account for substantial degradation of polytetrafluoroethylene, it also produces oxidized or peroxidized polytetrafluorethylene. Such polytetrafluoroethylene and polytetrafluoroethylene with free radicals still present must exist for at least several hours after irradiation. Post irradiation heat treatment consumes these peroxidized or free radical species of polytetrafluoroethylene and leads to further molecular weight reduction. Such free radical and peroxidation reactions are time/temperature dependent and are accelerated by exposure to elevated temperatures. The morphology of crystalline polymers as polytetrafluoroethylene can also be affected by exposure to elevated temperatures below their melt transition. Thus, it would appear that the post-irradiation heat treatment of polytetrafluoroethylene and perhaps even the concurrent heating of polytetrafluoroethylele while irradiating could have effects similar to annealling of the polymer. Such annealling could toughen the low molecular weight polytetrafluoroethylene to make it more grindable. However, if carried too far the annealled low molecular weight polytetrafluoroethylene could become too tough for a commercial piece of grinding equipment to replace it to a fine powder. Thus, excessive annealling could lead to grindable material, having, however, excessive large particles which cannot be easily broken down.
In the complex irradiation and heating processes discussed, both irradiation and thermally excited degradation processes are taking place. At the same time morphological changes due to an annealling type phenomena are also probably occurring. A desirable product can be formed by taking advantage of these competing changes in the polytetrafluoroethylene. The process conditions needed to achieve this are indicated in the above examples.
Based on the above, doses between 50 and 150 Mrads appear to be useful. Heat treatment can take place either concurrent with irradiation or subsequent to irradiation. The preferred temperature range appears to be between 120° C. (248° F.) and 288° C. (550° F.). Slightly higher temperatures could be used but can pose problems of melting and agglomeration as they approach the melting point of sintered polytetrafluoroethylene (327° C. or 621° F.) scrap.
Time of heating is a factor which is determined not only by effects on particle size but also the time required to remove from the plastic by diffusion through the plastic, of free fluorene liberated during the irradiation cycle. At present this latter factor has somewhat restricted the lower limit of processing times although processing times of one-half hour are believed to be valid to accomplish sufficient treatment of sintered polytetrafluoroethylene to permit grinding to fine powders.
Athough the process of the present invention is discussed in terms of electron beam irradiation; other sub-atomic particle irradiation such as from Cobalt 60 may be utilized.
Claims (19)
1. A process for rendering sintered polytetrafloroethylene capable of being ground to an average particle size of less than about 10 microns; the steps of which comprise:
subjecting sintered polytetrafluoroethylene in the presence of air or oxygen to ionizing radiation in the range of about 50 megarads to about 200 megarads, and
heating the sintered polytetrafluoroethylene in a range from about 150° F. to a temperature below the melting point of the material,
said radiation being conducted at a dose rate and said heating being conducted for a period of time sufficient to render said sintered polytetrafluoroethylene capable of being ground to an average particle size of less than about 10 microns.
2. A process according to claim 1 wherein heating and irradiating occur simultaneously.
3. A process according to claim 1 further including grinding and wherein heating, irradiation and grinding occur simultaneously.
4. A process according to claim 1 wherein sintered polytetrafluoroethylene is irradiated and then heated before a material loss of peroxidized and free radical species of polytetrafluoroethylene occurs.
5. A process according to claim 1 wherein said temperature range is 248° F. to 550° F.
6. A process according to claim 5 wherein the sintered polytetrafluoroethylene is held at temperature for at least about 2 hours.
7. A process according to claim 1 wherein the dose is approximately 90 megarads, the temperature is 500° F. and the material is held at temperature from about 2 hours to about 5 hours.
8. A sintered polytetrafluoroethylene material that has been treated by the process of claim 1.
9. A sintered polytetrafluoroethylene material that has been treated by the process of claims 2 or 3.
10. A sintered polytetrafluoroethylene material that has been treated by the process of claim 4.
11. A sintered polytetrafluoroethylene material that has been treated by the process of claims 5 or 6.
12. A sintered polytetrafluoroethylene material that has been treated by the process of claim 7.
13. An article of commerce comprising sintered polytetrafluoroethylene that has been subjected in the presence of air or oxygen to ionizing radiation in the range of about 50 megarads to about 200 megarads and to temperatures in a range from about 150° F. to a temperature below the melting point of the material.
14. An article of commerce according to claim 13 capable of being ground to an average particle size of 10 microns or less.
15. An article of commerce according to claim 13 wherein said article is in particulate form having an average particle size of 10 microns or less.
16. A process according to claim 1 wherein said radiation is conducted in a plurality of stages, the cumulative dosage amount of which resides in the range of about 50-200 megarads.
17. A process according to claim 16 wherein said radiation and heating are conducted simultaneously and said plurality of stages are each conducted at a dosage and rate to maintain said temperature within said range for said sufficient period of time.
18. A process according to claim 16 which includes alternating stages of radiation and aeration to maintain said temperature within said range for said sufficient period of time.
19. A process according to claim 1 which further includes grinding said sintered polytetrafloroethylene to an average particle size of 10 microns or less.
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/019,890 US4220511A (en) | 1979-03-12 | 1979-03-12 | Treatment of sintered poly-tetrafluoroethylene with irradiation and heat to produce a grindable material |
| CA346,865A CA1125699A (en) | 1979-03-12 | 1980-03-03 | Treatment of sintered polytetrafluoroethylene with irradiation and heat to produce a grindable material |
| EP19800300689 EP0017349B1 (en) | 1979-03-12 | 1980-03-06 | Treatment of sintered polytetrafluoroethylene with irradiation and heat to produce a grindable material |
| DE8080300689T DE3071646D1 (en) | 1979-03-12 | 1980-03-06 | Treatment of sintered polytetrafluoroethylene with irradiation and heat to produce a grindable material |
| ZA00801392A ZA801392B (en) | 1979-03-12 | 1980-03-10 | Treatment of sintered polytetrafluoro-ethylene with irradiation and heat to produce a grindable material |
| DK104080A DK104080A (en) | 1979-03-12 | 1980-03-11 | PROCEDURE FOR PUTTING THE POLYTETRAFLUORAETHYLE TO BE FORMED FOR SMALL PARTICLE SIZE |
| JP3150680A JPS55124612A (en) | 1979-03-12 | 1980-03-12 | Treating method for pulverizing burned polytetrafluoroethylene |
| BR8001476A BR8001476A (en) | 1979-03-12 | 1980-03-12 | TREATMENT OF SINTERIZED POLITETRAFLUOROETHYLENE WITH IRRADIATION AND HEAT TO PRODUCE A CRUSHABLE MATERIAL |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/019,890 US4220511A (en) | 1979-03-12 | 1979-03-12 | Treatment of sintered poly-tetrafluoroethylene with irradiation and heat to produce a grindable material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4220511A true US4220511A (en) | 1980-09-02 |
Family
ID=21795591
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/019,890 Expired - Lifetime US4220511A (en) | 1979-03-12 | 1979-03-12 | Treatment of sintered poly-tetrafluoroethylene with irradiation and heat to produce a grindable material |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US4220511A (en) |
| EP (1) | EP0017349B1 (en) |
| JP (1) | JPS55124612A (en) |
| BR (1) | BR8001476A (en) |
| CA (1) | CA1125699A (en) |
| DE (1) | DE3071646D1 (en) |
| DK (1) | DK104080A (en) |
| ZA (1) | ZA801392B (en) |
Cited By (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4451593A (en) * | 1981-03-31 | 1984-05-29 | Union Carbide Corporation | Process for finishing resin using reduced energy input |
| US4675380A (en) * | 1985-10-25 | 1987-06-23 | E. I. Du Pont De Nemours And Company | Melt-processible tetrafluoroethylene/perfluoroolefin copolymer granules and processes for preparing them |
| US4748005A (en) * | 1982-05-03 | 1988-05-31 | Shamrock Chemicals Corporation | Apparatus and method for radiation processing of materials |
| US4777192A (en) * | 1982-05-03 | 1988-10-11 | Shamrock Chemicals Corporation | Apparatus and method for radiation processing of materials |
| US4861408A (en) * | 1987-04-08 | 1989-08-29 | The United States Of America As Represented By The United States Department Of Energy | Modification of polymeric surface for improved adhesion via electron beam exposure |
| US4898779A (en) * | 1986-12-22 | 1990-02-06 | Daikin Industries Ltd. | Powders of tetrafluoroethylene copolymer and process for preparing the same |
| US5263256A (en) * | 1992-04-17 | 1993-11-23 | The Gillette Company | Method of treating razor blade cutting edges |
| US5296113A (en) * | 1990-02-26 | 1994-03-22 | Luniewski Robert S | Irradiation device for fluoropolymers |
| US5891573A (en) * | 1997-08-08 | 1999-04-06 | Shamrock Chemicals Corporation | Method of providing friable polytetrafluoroethylene products |
| WO2000034300A1 (en) * | 1998-12-09 | 2000-06-15 | Shamrock Technologies, Inc. | Continuous process for irradiating of polytetrafluoroethylene (ptfe) |
| CN1053846C (en) * | 1991-10-28 | 2000-06-28 | 吉莱特公司 | Coating cutting edges with fluorocarbon polymers |
| US6110532A (en) * | 1993-05-28 | 2000-08-29 | The Gillette Company | Method of coating cutting edges |
| US6228428B1 (en) | 1991-10-28 | 2001-05-08 | The Gillette Company | Coating cutting edges with fluorocarbon polymers |
| US6340718B1 (en) * | 2000-07-24 | 2002-01-22 | Steris Inc | Method of radiation treatment for fluoropolymer materials |
| US6433030B1 (en) * | 1997-10-31 | 2002-08-13 | E. I. Du Pont De Nemours And Company | Method for processing coating powder waste and coating powders thus obtained |
| US20020161067A1 (en) * | 2001-02-28 | 2002-10-31 | Japan Atomic Energy Research Institute | Radiation-modified poly (tetrafluoroethylene) resin feeds and a process for producing the same |
| US6486481B1 (en) | 1999-11-12 | 2002-11-26 | Ausimont Usa, Inc. | Vibratory table apparatus and associated equipment and methods for radiation treatment of polymeric materials |
| WO2003106540A2 (en) * | 2002-03-14 | 2003-12-24 | Shamrock Technologies, Inc. | Methods for producing submicron polytetrafluoroethylene powder and products thereof |
| US20040266986A1 (en) * | 2003-06-26 | 2004-12-30 | Alberg Michele J | Polytetrafluoroethylene treatment |
| US20070244212A1 (en) * | 2003-10-30 | 2007-10-18 | Dieter Lehmann | Modified Perfluoroplastics, and Method for The Production Thereof |
| US20070282031A1 (en) * | 2003-10-30 | 2007-12-06 | Dieter Lehmann | Radically Coupled Ptfe Polymer Powders, and Method for the Production Thereof |
| US20080293843A1 (en) * | 2005-11-28 | 2008-11-27 | The Surrey Technology Centre. | Comminutable Polyesters |
| US20090105436A1 (en) * | 2003-10-30 | 2009-04-23 | Dieter Lehmann | Radically coupled ptfe polymer compounds and method for the production thereof |
| DE102014222283A1 (en) * | 2014-10-31 | 2016-05-04 | Aktiebolaget Skf | Plastic self-lubricating bearing cage |
| EP3385309A4 (en) * | 2016-08-04 | 2019-06-12 | Daikin Industries, Ltd. | Method for producing low molecular weight polytetrafluoroethylene, low molecular weight polytetrafluoroethylene, and powder |
| US10703867B2 (en) | 2016-06-10 | 2020-07-07 | E-Beam Services, Inc. | Thermal treatment of irradiated material solids using a heat transfer liquid |
| US11548989B2 (en) * | 2018-02-07 | 2023-01-10 | Daikin Industries, Ltd. | Method for producing composition containing low molecular weight polytetrafluoroethylene |
| EP4031620A4 (en) * | 2019-09-19 | 2023-10-11 | Gujarat Fluorochemicals Limited | An extrusion process for preparing a low molecular weight polytetrafluoroethylene micropowder |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2119385B (en) * | 1982-05-03 | 1985-12-18 | Shamrock Chemicals Corp | Apparatus and method for radiation processing of materials |
| JP3317452B2 (en) * | 1992-10-05 | 2002-08-26 | 株式会社レイテック | Modified polytetrafluoroethylene and method for producing the same |
| US10648496B2 (en) | 2017-06-28 | 2020-05-12 | Blanking Systems, Inc. | Mount |
| WO2019156071A1 (en) | 2018-02-07 | 2019-08-15 | ダイキン工業株式会社 | Method for producing composition containing low molecular weight polytetrafluoroethylene |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3766031A (en) * | 1972-04-10 | 1973-10-16 | Garlock Inc | Process for non-destructive radiation degradation of polytetrafluoroethylene |
| US3878164A (en) * | 1971-07-02 | 1975-04-15 | Ici Ltd | Tetrafluoroethylene polymer compositions |
| US4029870A (en) * | 1970-02-03 | 1977-06-14 | Imperial Chemical Industries Limited | Tetrafluoroethylene polymers |
| US4036718A (en) * | 1970-02-03 | 1977-07-19 | Imperial Chemical Industries Limited | Process for preparing a friable tetrafluoroethylene polymer powder from unsintered coagulated dispersion grade tetrafluoroethylene polymer |
| US4052278A (en) * | 1970-02-03 | 1977-10-04 | Imperial Chemical Industries Limited | Finely divided, irradiated tetrafluorethylene polymers |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5225858B2 (en) * | 1972-06-22 | 1977-07-11 |
-
1979
- 1979-03-12 US US06/019,890 patent/US4220511A/en not_active Expired - Lifetime
-
1980
- 1980-03-03 CA CA346,865A patent/CA1125699A/en not_active Expired
- 1980-03-06 EP EP19800300689 patent/EP0017349B1/en not_active Expired
- 1980-03-06 DE DE8080300689T patent/DE3071646D1/en not_active Expired
- 1980-03-10 ZA ZA00801392A patent/ZA801392B/en unknown
- 1980-03-11 DK DK104080A patent/DK104080A/en not_active Application Discontinuation
- 1980-03-12 JP JP3150680A patent/JPS55124612A/en active Pending
- 1980-03-12 BR BR8001476A patent/BR8001476A/en unknown
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4029870A (en) * | 1970-02-03 | 1977-06-14 | Imperial Chemical Industries Limited | Tetrafluoroethylene polymers |
| US4036718A (en) * | 1970-02-03 | 1977-07-19 | Imperial Chemical Industries Limited | Process for preparing a friable tetrafluoroethylene polymer powder from unsintered coagulated dispersion grade tetrafluoroethylene polymer |
| US4052278A (en) * | 1970-02-03 | 1977-10-04 | Imperial Chemical Industries Limited | Finely divided, irradiated tetrafluorethylene polymers |
| US3878164A (en) * | 1971-07-02 | 1975-04-15 | Ici Ltd | Tetrafluoroethylene polymer compositions |
| US3766031A (en) * | 1972-04-10 | 1973-10-16 | Garlock Inc | Process for non-destructive radiation degradation of polytetrafluoroethylene |
Cited By (51)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4451593A (en) * | 1981-03-31 | 1984-05-29 | Union Carbide Corporation | Process for finishing resin using reduced energy input |
| US4748005A (en) * | 1982-05-03 | 1988-05-31 | Shamrock Chemicals Corporation | Apparatus and method for radiation processing of materials |
| US4777192A (en) * | 1982-05-03 | 1988-10-11 | Shamrock Chemicals Corporation | Apparatus and method for radiation processing of materials |
| US4675380A (en) * | 1985-10-25 | 1987-06-23 | E. I. Du Pont De Nemours And Company | Melt-processible tetrafluoroethylene/perfluoroolefin copolymer granules and processes for preparing them |
| US4898779A (en) * | 1986-12-22 | 1990-02-06 | Daikin Industries Ltd. | Powders of tetrafluoroethylene copolymer and process for preparing the same |
| US4977221A (en) * | 1986-12-22 | 1990-12-11 | Daikin Industries, Ltd. | Powders of tetrafluoroethylene copolymer and process for preparing the same |
| US4861408A (en) * | 1987-04-08 | 1989-08-29 | The United States Of America As Represented By The United States Department Of Energy | Modification of polymeric surface for improved adhesion via electron beam exposure |
| US5296113A (en) * | 1990-02-26 | 1994-03-22 | Luniewski Robert S | Irradiation device for fluoropolymers |
| CN1053846C (en) * | 1991-10-28 | 2000-06-28 | 吉莱特公司 | Coating cutting edges with fluorocarbon polymers |
| US6228428B1 (en) | 1991-10-28 | 2001-05-08 | The Gillette Company | Coating cutting edges with fluorocarbon polymers |
| US5263256A (en) * | 1992-04-17 | 1993-11-23 | The Gillette Company | Method of treating razor blade cutting edges |
| US6110532A (en) * | 1993-05-28 | 2000-08-29 | The Gillette Company | Method of coating cutting edges |
| US5891573A (en) * | 1997-08-08 | 1999-04-06 | Shamrock Chemicals Corporation | Method of providing friable polytetrafluoroethylene products |
| US6433030B1 (en) * | 1997-10-31 | 2002-08-13 | E. I. Du Pont De Nemours And Company | Method for processing coating powder waste and coating powders thus obtained |
| WO2000034300A1 (en) * | 1998-12-09 | 2000-06-15 | Shamrock Technologies, Inc. | Continuous process for irradiating of polytetrafluoroethylene (ptfe) |
| US6486481B1 (en) | 1999-11-12 | 2002-11-26 | Ausimont Usa, Inc. | Vibratory table apparatus and associated equipment and methods for radiation treatment of polymeric materials |
| US6764657B2 (en) | 2000-07-24 | 2004-07-20 | Steris Inc. | Apparatus for irradiating for fluoropolymer materials |
| US6340718B1 (en) * | 2000-07-24 | 2002-01-22 | Steris Inc | Method of radiation treatment for fluoropolymer materials |
| US20020161067A1 (en) * | 2001-02-28 | 2002-10-31 | Japan Atomic Energy Research Institute | Radiation-modified poly (tetrafluoroethylene) resin feeds and a process for producing the same |
| US6762215B2 (en) * | 2001-02-28 | 2004-07-13 | Japan Atomic Energy Research | Radiation-modified poly(tetrafluoroethylene) resin feeds and a process for producing the same |
| US7220799B2 (en) | 2001-02-28 | 2007-05-22 | Japan Atomic Energy Research Institute | Radiation-modified poly (tetrafluoroethylene) resin feeds and a process for producing the same |
| US20040220294A1 (en) * | 2001-02-28 | 2004-11-04 | Japan Atomic Energy Research Institute | Radiation-modified poly (tetrafluoroethylene) resin feeds and a process for producing the same |
| WO2003106540A2 (en) * | 2002-03-14 | 2003-12-24 | Shamrock Technologies, Inc. | Methods for producing submicron polytetrafluoroethylene powder and products thereof |
| WO2003106540A3 (en) * | 2002-03-14 | 2004-05-13 | Shamrock Tech Inc | Methods for producing submicron polytetrafluoroethylene powder and products thereof |
| US7482393B2 (en) * | 2002-03-14 | 2009-01-27 | Shamrock Technologies Inc. | Methods for producing submicron polytetrafluoroethylene powder and products thereof |
| US20060020072A1 (en) * | 2002-03-14 | 2006-01-26 | Cody Charles A | Methods for producing submicron polytetrafluoroethylene powder and products thereof |
| US20040266986A1 (en) * | 2003-06-26 | 2004-12-30 | Alberg Michele J | Polytetrafluoroethylene treatment |
| US7335721B2 (en) * | 2003-06-26 | 2008-02-26 | Advanced Technology Materials, Inc. | Polytetrafluoroethylene treatment |
| US7067616B2 (en) * | 2003-06-26 | 2006-06-27 | Advanced Technology Materials, Inc. | Polytetrafluoroethylene treatment |
| US20060235197A1 (en) * | 2003-06-26 | 2006-10-19 | Alberg Michele J | Polytetrafluoroethylene treatment |
| WO2005003189A1 (en) * | 2003-06-26 | 2005-01-13 | Advanced Technology Materials, Inc. | Polytetrafluoroethylene treatment |
| US20100298461A1 (en) * | 2003-10-30 | 2010-11-25 | Leibniz-Institut Fuer Polymerforschung Dreseden E. V. | Radically Coupled PTFE Polymer Powder and Method for the Production Thereof |
| US8030367B2 (en) * | 2003-10-30 | 2011-10-04 | Leibniz-Institut Fuer Polymerforschung Dresden E.V. | Radically coupled PTFE polymer powder and method for the production thereof |
| US20070282031A1 (en) * | 2003-10-30 | 2007-12-06 | Dieter Lehmann | Radically Coupled Ptfe Polymer Powders, and Method for the Production Thereof |
| US20090105436A1 (en) * | 2003-10-30 | 2009-04-23 | Dieter Lehmann | Radically coupled ptfe polymer compounds and method for the production thereof |
| US8648149B2 (en) | 2003-10-30 | 2014-02-11 | Leibniz-Institut Fuer Polymerforschung Dresden E.V. | Radically coupled PTFE polymer compounds and method for the production thereof |
| US7759441B2 (en) | 2003-10-30 | 2010-07-20 | Leibniz-Institut Fuer Polymerforschung Dresden E.V. | Radically coupled PTFE polymer compounds and method for the production thereof |
| US7790780B2 (en) * | 2003-10-30 | 2010-09-07 | Leibniz-Institut Fuer Polymerforschung Dresden E.V. | Radically coupled PTFE polymer powders, and method for the production thereof |
| US20100249333A1 (en) * | 2003-10-30 | 2010-09-30 | Leibniz-Institut Fuer Polymerforschung Dresden E.V. | Radically coupled ptfe polymer compounds and method for the production thereof |
| US20070244212A1 (en) * | 2003-10-30 | 2007-10-18 | Dieter Lehmann | Modified Perfluoroplastics, and Method for The Production Thereof |
| US20080293843A1 (en) * | 2005-11-28 | 2008-11-27 | The Surrey Technology Centre. | Comminutable Polyesters |
| US8101675B2 (en) | 2005-11-28 | 2012-01-24 | Cleansors Limited | Comminutable polyesters |
| GB2446764B (en) * | 2005-11-28 | 2010-06-09 | Cleansorb Ltd | Comminutable polyesters |
| DE102014222283A1 (en) * | 2014-10-31 | 2016-05-04 | Aktiebolaget Skf | Plastic self-lubricating bearing cage |
| US10703867B2 (en) | 2016-06-10 | 2020-07-07 | E-Beam Services, Inc. | Thermal treatment of irradiated material solids using a heat transfer liquid |
| EP3385309A4 (en) * | 2016-08-04 | 2019-06-12 | Daikin Industries, Ltd. | Method for producing low molecular weight polytetrafluoroethylene, low molecular weight polytetrafluoroethylene, and powder |
| EP3643745A3 (en) * | 2016-08-04 | 2020-07-22 | Daikin Industries, Limited | Powder comprising low molecular weight polytetrafluoroethylene and uses thereof |
| US10870735B2 (en) | 2016-08-04 | 2020-12-22 | Daikin Industries, Ltd. | Method for producing low molecular weight polytetrafluoroethylene, low molecular weight polytetrafluoroethylene, and powder |
| US11814490B2 (en) | 2016-08-04 | 2023-11-14 | Daikin Industries, Ltd. | Method for producing low molecular weight polytetrafluoroethylene, low molecular weight polytetrafluoroethylene, and powder |
| US11548989B2 (en) * | 2018-02-07 | 2023-01-10 | Daikin Industries, Ltd. | Method for producing composition containing low molecular weight polytetrafluoroethylene |
| EP4031620A4 (en) * | 2019-09-19 | 2023-10-11 | Gujarat Fluorochemicals Limited | An extrusion process for preparing a low molecular weight polytetrafluoroethylene micropowder |
Also Published As
| Publication number | Publication date |
|---|---|
| BR8001476A (en) | 1980-11-11 |
| ZA801392B (en) | 1981-03-25 |
| DE3071646D1 (en) | 1986-07-24 |
| EP0017349A1 (en) | 1980-10-15 |
| CA1125699A (en) | 1982-06-15 |
| EP0017349B1 (en) | 1986-06-18 |
| DK104080A (en) | 1980-09-13 |
| JPS55124612A (en) | 1980-09-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4220511A (en) | Treatment of sintered poly-tetrafluoroethylene with irradiation and heat to produce a grindable material | |
| CA1184728A (en) | Continuous process for the agglomeration of ptfe powders in a liquid medium, and modified ptfe powder obtained thereby | |
| US3766031A (en) | Process for non-destructive radiation degradation of polytetrafluoroethylene | |
| DE60018467T2 (en) | TREATMENT OF POLYMER FOAM | |
| US3766133A (en) | Polytetrafluoroethylene filled and unfilled molding powders and theirpreparation | |
| US5916929A (en) | Method for irradiating organic polymers | |
| US4508859A (en) | Finishing of rotational molding grade resin | |
| US3997494A (en) | Compounded thermoplastic polymeric materials and fillers | |
| EP3564295A1 (en) | Method for preparing super absorbent polymer | |
| US3781258A (en) | Polytetrafluoroethylene powder and method of preparation thereof | |
| US5411213A (en) | Method for treatment of solid materials | |
| US4045403A (en) | Method of compounding thermo-plastic polymeric materials and fillers | |
| EP1001880B1 (en) | Method of providing friable polytetrafluoroethylene products | |
| Herzig et al. | Correlations between image-analysed morphology and mechanical properties of calcium carbonate-filled polypropylene | |
| US3895121A (en) | Processing of wheat germ to retard rancidification | |
| US2966468A (en) | Process of reclaiming scrap vulcanized rubber | |
| JP2006527269A (en) | Method for producing submicron polytetrafluoroethylene powder and product thereof | |
| CH429125A (en) | Process for fine grinding of plastics or synthetic resins | |
| DE2161857C3 (en) | Process for the production of a polytetrafluoroethylene molding powder optionally provided with fillers | |
| DE2315942A1 (en) | Free flowing polytetrafluoroethylene prepn - by granulation with a liquid | |
| Dong et al. | Radiation effects on the immiscible polymer blend of nylon1010 and high-impact strength polystyrene (II): mechanical properties and morphology | |
| JP2022501240A (en) | Polymer powder and its preparation method | |
| AT525907B1 (en) | Process for processing polycondensates | |
| US2676168A (en) | Method of producing a food product from scrap particles of hide | |
| JPH0491134A (en) | Pulverization of polymer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: RADIATION DYNAMICS, INC., SOUTH SERVICE ROAD, MELV Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:RADIATION DYNAMICS, INC., A NY CORP;REEL/FRAME:004270/0694 Effective date: 19840524 |
|
| AS | Assignment |
Owner name: CITICORP INDUSTRIAL CREDIT, INC., 560 SYLVAN AVENU Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:E-BEAM SERVICES, INC.,;REEL/FRAME:004533/0710 Effective date: 19860325 |
|
| AS | Assignment |
Owner name: RADIATION DYNAMICS, INC., 316 SOUTH SERVICE RD., M Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:RADIATION DYNAMICS, INC., A CORP. OF DE.;REEL/FRAME:004682/0418 Effective date: 19870311 |
|
| AS | Assignment |
Owner name: MEDICAL STERILIZATION, INC., NEW YORK Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:RADIATION DYNAMICS, INC.;REEL/FRAME:006253/0638 Effective date: 19920902 |